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1.发明授权Counter-current catalyst flow with split feed and two reactor train processing 有权逆流催化剂流动与分流进料和两个反应堆列车加工公开(公告)号：US08882994B2
公开(公告)日：2014-11-11
申请号：US13327164
申请日：2011-12-15
申请人： Mark D. Moser , David A. Wegerer , Kurt M. VandenBussche , Manuela Serban , Mark P. Lapinski , Mary Jo Wier , Gregory J. Gajda
发明人： Mark D. Moser , David A. Wegerer , Kurt M. VandenBussche , Manuela Serban , Mark P. Lapinski , Mary Jo Wier , Gregory J. Gajda
IPC分类号： C10G35/04
CPC分类号： C10G59/02 , C10G59/06 , C10G2400/30
摘要： A process is presented for the increasing the yields of aromatics from reforming a hydrocarbon feedstream. The process includes splitting a naphtha feedstream into a light hydrocarbon stream, and a heavier stream having a relatively rich concentration of naphthenes. The heavy stream is reformed to convert the naphthenes to aromatics and the resulting product stream is further reformed with the light hydrocarbon stream to increase the aromatics yields. The process includes passing a catalyst stream in a counter-current flow relative to the hydrocarbon process stream.
摘要翻译： 提出了一种从碳氢化合物原料流重整提高芳族化合物产率的方法。 该方法包括将石脑油进料流分解成轻质烃物流，以及将较稠油的浓度较高的环烷烃。 将重质流重整以将环烷烃转化为芳族化合物，并且所得产物流用轻质烃流进一步重整以提高芳烃产率。 该方法包括使相对于烃工艺物流的逆流流动催化剂流。
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公开(公告)号：US08845884B2
公开(公告)日：2014-09-30
申请号：US13417203
申请日：2012-03-10
申请人： Gregory J. Gajda , Mary Jo Wier , Mark P. Lapinski , David A. Wegerer , Kurt M. VandenBussche , Mark D. Moser
发明人： Gregory J. Gajda , Mary Jo Wier , Mark P. Lapinski , David A. Wegerer , Kurt M. VandenBussche , Mark D. Moser
IPC分类号： C10G35/04 , C10G59/06 , C10G35/06 , C10G35/085
CPC分类号： C10G35/04 , C10G35/06 , C10G35/065 , C10G35/085 , C10G59/06 , C10G2300/1044 , C10G2400/30
摘要： A process for reforming a hydrocarbon stream is presented. The process involves splitting a naphtha feedstream to at least two feedstreams and passing each feedstream to separation reformers. The reformers are operated under different conditions to utilize the differences in the reaction properties of the different hydrocarbon components. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.
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3.发明授权Co-current catalyst flow with feed for fractionated feed recombined and sent to high temperature reforming reactors 有权用于分批进料的进料的电流催化剂流重新混合并送至高温重整反应器公开(公告)号：US09024099B2
公开(公告)日：2015-05-05
申请号：US13327200
申请日：2011-12-15
摘要： A process is presented for the increasing the yields of aromatics from reforming a hydrocarbon feedstream. The process includes splitting a naphtha feedstream into a light hydrocarbon stream, and a heavier stream having a relatively rich concentration of naphthenes. The heavy stream is reformed to convert the naphthenes to aromatics and the resulting product stream is further reformed with the light hydrocarbon stream to increase the aromatics yields. The catalyst is passed through the reactors in a sequential manner.
摘要翻译： 提出了一种从碳氢化合物原料流重整提高芳族化合物产率的方法。 该方法包括将石脑油进料流分解成轻质烃物流，以及将较稠油的浓度较高的环烷烃。 将重质流重整以将环烷烃转化为芳族化合物，并且所得产物流用轻质烃流进一步重整以提高芳烃产率。 催化剂以顺序的方式通过反应器。
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公开(公告)号：US08845883B2
公开(公告)日：2014-09-30
申请号：US13417181
申请日：2012-03-09
CPC分类号： C10G59/00 , C10G2300/1044 , C10G2400/02 , C10G2400/30
摘要： A process for reforming a hydrocarbon stream is presented. The process involves splitting a naphtha feedstream to at least two feedstreams and passing each feedstream to separation reformers. The reformers are operated under different conditions to utilize the differences in the reaction properties of the different hydrocarbon components. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.
摘要翻译： 提出了一种重整烃流的方法。 该方法包括将石脑油进料流分成至少两个进料流并将每个进料流通过分离重整器。 改性剂在不同条件下运行，以利用不同烃组分的反应性质的差异。 该方法利用普通的催化剂和用于回收生成的所需芳族化合物的常见的下游方法。
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公开(公告)号：US08926829B2
公开(公告)日：2015-01-06
申请号：US13416513
申请日：2012-03-09
申请人： Manuela Serban , Antoine Negiz , Kurt M. VandenBussche , Mark D. Moser , David A. Wegerer , Gregory J. Gajda
发明人： Manuela Serban , Antoine Negiz , Kurt M. VandenBussche , Mark D. Moser , David A. Wegerer , Gregory J. Gajda
IPC分类号： C10G35/04 , C10G35/06 , C10G35/085 , C10G59/06
CPC分类号： C10G35/04 , C10G35/06 , C10G35/065 , C10G35/085 , C10G59/06 , C10G2300/1044 , C10G2400/30
摘要： A process for reforming a hydrocarbon stream is presented. The process involves splitting a naphtha feedstream to at least two feedstreams and passing each feedstream to separation reformers. The reformers are operated under different conditions to utilize the differences in the reaction properties of the different hydrocarbon components. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.
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公开(公告)号：US08906226B2
公开(公告)日：2014-12-09
申请号：US13417202
申请日：2012-03-09
IPC分类号： C10G35/04 , C10G35/085 , C10G59/00
CPC分类号： C10G59/00 , C10G2300/1044 , C10G2400/02 , C10G2400/30
摘要： A process for reforming a hydrocarbon stream is presented. The process involves splitting a naphtha feedstream to at least two feedstreams and passing each feedstream to separation reformers. The reformers are operated under different conditions to utilize the differences in the reaction properties of the different hydrocarbon components. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.
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公开(公告)号：US20120277505A1
公开(公告)日：2012-11-01
申请号：US13416513
申请日：2012-03-09
申请人： Manuela Serban , Antoine Negiz , Kurt M. VandenBussche , Mark D. Moser , David A. Wegerer , Gregory J. Gajda
发明人： Manuela Serban , Antoine Negiz , Kurt M. VandenBussche , Mark D. Moser , David A. Wegerer , Gregory J. Gajda
IPC分类号： C07C7/00
CPC分类号： C10G35/04 , C10G35/06 , C10G35/065 , C10G35/085 , C10G59/06 , C10G2300/1044 , C10G2400/30
摘要： A process for reforming a hydrocarbon stream is presented. The process involves splitting a naphtha feedstream to at least two feedstreams and passing each feedstream to separation reformers. The reformers are operated under different conditions to utilize the differences in the reaction properties of the different hydrocarbon components. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.
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公开(公告)号：US20120275974A1
公开(公告)日：2012-11-01
申请号：US13440527
申请日：2012-04-05
IPC分类号： B01J19/00
CPC分类号： C01B3/26 , B01J8/008 , B01J8/0415 , B01J8/0492 , B01J8/0496 , B01J2208/00194 , B01J2208/0053 , B01J2219/024 , C01B2203/0277
摘要： An apparatus for reforming a hydrocarbon stream is presented. The apparatus involves changing the design of reformers and associated equipment to allow for increasing the processing temperatures in the reformers and heaters. The reformers are operated under different conditions to utilize advantages in the equilibriums, but require modifications to prevent increasing thermal cracking and to prevent increases in coking.
摘要翻译： 提出了一种用于重整烃流的装置。 该设备包括改变重整器和相关设备的设计，以允许提高重整器和加热器中的加工温度。 改造者在不同条件下运行，以利用平衡中的优点，但需要进行修改以防止增加热裂解并防止焦化增加。
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公开(公告)号：US09023298B2
公开(公告)日：2015-05-05
申请号：US13440527
申请日：2012-04-05
IPC分类号： B01J8/00 , B01J8/04 , B01J19/00 , B01J19/24 , C01B3/00 , C01B3/02 , C01B3/22 , C01B3/24 , C01B3/26 , C01B3/32 , C01B3/34 , C01B3/38
CPC分类号： C01B3/26 , B01J8/008 , B01J8/0415 , B01J8/0492 , B01J8/0496 , B01J2208/00194 , B01J2208/0053 , B01J2219/024 , C01B2203/0277
摘要： An apparatus for reforming a hydrocarbon stream is presented. The apparatus involves changing the design of reformers and associated equipment to allow for increasing the processing temperatures in the reformers and heaters. The reformers are operated under different conditions to utilize advantages in the equilibriums, but require modifications to prevent increasing thermal cracking and to prevent increases in coking.
摘要翻译： 提出了一种用于重整烃流的装置。 该设备包括改变重整器和相关设备的设计，以允许提高重整器和加热器中的加工温度。 改造者在不同条件下运行，以利用平衡中的优点，但需要进行修改以防止增加热裂解并防止焦化增加。
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公开(公告)号：US20120277500A1
公开(公告)日：2012-11-01
申请号：US13440487
申请日：2012-04-05
IPC分类号： C07C2/00
CPC分类号： C10G35/04 , C07C4/06 , C10G35/06 , C10G61/04 , C10G2300/1044 , C10G2300/4018 , C10G2400/30 , Y02P20/584 , C07C15/02 , C07C15/067
摘要： A process for reforming a hydrocarbon stream is presented. The process involves increasing the processing temperatures in the reformers. The reformers are operated under different conditions to utilize advantages in the equilibriums, but require modifications to prevent increasing thermal cracking and to prevent increases in coking. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.
摘要翻译： 提出了一种重整烃流的方法。 该方法涉及提高改性剂中的加工温度。 改造者在不同条件下运行，以利用平衡中的优点，但需要进行修改以防止增加热裂解并防止焦化增加。 该方法利用普通的催化剂和用于回收生成的所需芳族化合物的常见的下游方法。
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